CN211311151U - Experiment effluent disposal system - Google Patents
Experiment effluent disposal system Download PDFInfo
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- CN211311151U CN211311151U CN201922166698.5U CN201922166698U CN211311151U CN 211311151 U CN211311151 U CN 211311151U CN 201922166698 U CN201922166698 U CN 201922166698U CN 211311151 U CN211311151 U CN 211311151U
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Abstract
The utility model relates to an experiment effluent disposal system technical field just discloses an experiment effluent disposal system, including source water tank, source water tank's outlet department leads to pipe one and connects active water pump, and source water pump's output port leads to pipe two to be connected with the catalysis pond, and the intercommunication has branch pipe one, branch pipe two, branch pipe three and branch pipe four on the water pipe two in proper order, and manual ball valve one, solenoid valve one, rotor formula flowmeter and manometer are installed in proper order to water pipe two from source water pump's one end. The utility model discloses make the homogeneous mixing purify the liquid medicine in the experiment waste water, filter the waste water that filters and lead to the purification treatment that circulates in the catalysis pond once more, carry out stronger effect of killing to various bacterium and virus in the experiment waste water, ozone gas has effects such as very strong oxidation, catalysis simultaneously, effectively improves the reaction rate between liquid medicine and the waste water, the dull and stereotyped membrane of pottery carries out effective filtration purification to the small non-sedimentary suspended particles thing in the catalysis pond, and then ensures entire system purification treatment's quality.
Description
Technical Field
The utility model relates to an experiment effluent disposal system technical field specifically is an experiment effluent disposal system.
Background
The traditional laboratory wastewater is usually directly discharged to a sewer, and different laboratories may contain chemical agents, animal organs and the like, which are directly discharged to a water body, pollution to water resources is caused, the environment is influenced, along with the continuous enhancement of environmental awareness of people, the purification treatment of the experimental water is correspondingly improved, the pollution of the experimental wastewater to the environment is greatly reduced, the existing experimental wastewater is generally subjected to catalytic reaction and precipitation by mixing simple liquid medicine in a reaction tank, the aim of purifying the experimental wastewater is fulfilled, however, the treatment method can not effectively purify some harmful substances, the treated wastewater can still cause certain influence on the environment, therefore, the inventor designs a novel test wastewater treatment system, and the test wastewater is treated by a multiple circulation process, so that the quality of the discharged water of the test is purified to the maximum extent.
SUMMERY OF THE UTILITY MODEL
The problem of experimental waste water through simple liquid medicine mixing catalysis can not effectually purify the harmful material in the waste water is solved.
The utility model provides an experiment effluent disposal system, including the source water tank, the outlet department of source water tank leads to pipe one and connects active water pump, the output port of source water pump leads to pipe two to be connected with the catalysis pond, it has branch pipe one to communicate in proper order on the pipe two, branch pipe three and branch pipe four, manual ball valve one is installed in proper order from the one end of source water pump to pipe two, solenoid valve one, rotor type flowmeter and manometer, branch pipe one, branch pipe two, branch pipe three and the four terminal departments of branch pipe have connected gradually PE charge device, flocculating agent charge device, PAM charge device and PAC charge device.
The bottom one side drain port department of catalysis pond has the sludge pump through water pipe three connections, and the output of sludge pump leads to the mud filter bag of four fixed intercommunications of water pipe, installs manometer one on the water pipe four, and the outlet department of mud filter bag leads to pipe five to be linked together with the catalysis pond, and check valve one and solenoid valve two are installed in proper order from the one end in catalysis pond on the water pipe three, install manual ball valve two on the water pipe four.
The other water outlet on one side of the bottom of the catalysis tank is connected with a gas-liquid mixing pump through a water pipe six, one output port of the gas-liquid mixing pump is communicated with a sludge filter bag through a water pipe seven, a manual ball valve three and a pressure gauge two are installed on the water pipe seven, a gas input port of the gas-liquid mixing pump is connected with an ozone generator through a water pipe eight, a pressure gauge three is installed on the water pipe eight, a cooling input port of the ozone generator is connected with an output port of the ozone generator respectively, the water pipe nine is far away from the ozone generator and is connected with a ceramic flat membrane, the other end of the water pipe ten is a tap water inlet, the other input port of the ceramic flat membrane is communicated with the bottom of the catalysis tank through a water pipe eleven, and a check valve two.
The output port of the ceramic flat membrane is connected with a standard water pump through a water pipe twelve, a pressure protection switch is installed on the water pipe twelve, the output port of the standard water pump is connected with a standard water tank through a water pipe thirteen, and a solenoid valve four is installed on the water pipe thirteen.
Preferably, flow pumps are fixedly installed at the output liquid guide ports of the PE dosing device, the flocculating agent dosing device, the PAM dosing device and the PAC dosing device, and the output ports of the flow pumps are respectively communicated with a branch pipe I, a branch pipe II, a branch pipe III and a branch pipe IV which correspond to each other.
Preferably, the tap water inlet injects cooling liquid into the ozone generator through a water pipe ten for circulation, and the circulated cooling water is introduced into the ceramic flat membrane through a water pipe nine.
Preferably, a liquid level switch for detecting the height of the water level is arranged at the top of the source water tank.
Preferably, a liquid level switch II for detecting the height of the water level is arranged at the top of the standard-reaching water tank.
Compared with the prior art:
(1) this experiment effluent disposal system mutually supports through setting up PE charge device, flocculating agent charge device, PAM charge device and PAC charge device, carries out substep ration medicine with the experimental water of deriving in to source water tank 1 through corresponding constant delivery pump for source water is well misce bene and is purified the liquid medicine, carries out reaction catalysis in the direct leading-in catalytic pool of water pipe two, and the effectual purification efficiency who improves the purification liquid medicine.
(2) This experiment effluent disposal system mutually supports through setting up sludge pump and mud filter bag, and when equipment uses, produced solid-state debris are taken out through the sludge pump through liquid medicine reaction sedimentation in the catalysis pond, filter in four leading-in mud filter bags of water pipe for fixed debris are filtered, and the waste water that filters goes out is leading-in catalysis pond again and is circulated purification treatment, thereby effectual harmful impurity with in the experiment waste water carries out abundant reflection and purifies.
(3) This experiment effluent disposal system, mutually support through setting up gas-liquid mixing pump and ozone generator, when equipment uses, decompose out ozone in the ozone generator and pass through in the leading-in catalytic pool of gas-liquid mixing pump, thereby the ozone content in the effectual increase catalytic pool, and then carry out stronger killing effect to various bacterium in the experiment waste water and virus, ozone gas has very strong oxidation simultaneously, effect such as catalysis, effectively improve the reaction rate between liquid medicine and the waste water, and then guarantee waste water purification treatment's quality, the leading-in cooling running water of running water inlet department carries out the heat exchange cooling to ozone generator inside here simultaneously, guarantee the stability of complex between each mechanism.
(4) This experiment effluent disposal system will carry out filtration treatment once more from the water purification of deriving in the catalytic tank through setting up the dull and stereotyped membrane of pottery, carries out effective filtration purification to the small suspended particles who does not deposit in the catalytic tank, and then ensures entire system purification treatment's quality.
Drawings
Fig. 1 is a schematic flow chart of the present invention.
In the figure: the device comprises a 1-source water tank, a 2-source water pump, a 3-catalysis tank, a 4PE dosing device, a 5-flocculant dosing device, a 6PAM dosing device, a 7PAC dosing device, an 8 sludge pump, a 9 sludge filter bag, a 10 ceramic flat membrane, an 11 standard water pump, a 12 standard water tank, a 13 gas-liquid mixing pump, a 14 ozone generator and a 15 tap water inlet.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
As shown in fig. 1, the utility model provides a technical solution: an experimental wastewater treatment system comprises a source water tank 1, a first liquid level switch for detecting the height of a water level is arranged at the top of the source water tank 1, a first water outlet of the source water tank 1 is connected with an active water pump 2 through a first water pipe, an output port of the source water pump 2 is connected with a catalytic pool 3 through a second water pipe, the second water pipe is sequentially communicated with a first branch pipe, a second branch pipe, a third branch pipe and a fourth branch pipe, the second water pipe is sequentially provided with a first manual ball valve, a first electromagnetic valve, a rotor type flowmeter and a pressure gauge from one end of the source water pump 2, the flow direction and the flow rate of the first manual ball valve and the second electromagnetic valve are effectively controlled, the rotor type flowmeter and the pressure gauge are arranged to increase the control of relevant operators on the treatment system, and the tail ends of the first branch pipe, the second branch pipe, the third branch pipe and the fourth branch pipe are sequentially and fixedly connected with a PE, flow pumps are fixedly installed at output liquid guide ports of the PE dosing device 4, the flocculating agent dosing device 5, the PAM dosing device 6 and the PAC dosing device 7, output ports of the flow pumps are respectively communicated with a branch pipe I, a branch pipe II, a branch pipe III and a branch pipe IV which correspond to the branch pipes I, the branch pipe II and the branch pipe III correspondingly, an acidity blender is added into the PE dosing device 4, an alkalinity blender is added into the flocculating agent dosing device 5, a PAM dilute-release agent is added into the PAM dosing device, a PAC dilute-release agent is added into the PAC dosing device 7, the experiment wastewater can be enabled to fully react with various agents and neutralize the acidity and alkalinity, and impurities in the experiment wastewater are.
The bottom one side drain port department of catalysis pond 3 is connected with sludge pump 8 through water pipe three, and sludge pump 8's output leads to the mud filter bag 9 of four fixed intercommunications of water pipe, installs manometer one on the water pipe four, and the outlet department of mud filter bag 9 leads to pipe five to be linked together with catalysis pond 3, installs check valve one and solenoid valve two from the one end in proper order in catalysis pond 3 on the water pipe three, installs manual ball valve two on the water pipe four.
The other water outlet on one side of the bottom of the catalysis tank 3 is connected with a gas-liquid mixing pump 13 through a water pipe six, one output port of the gas-liquid mixing pump 13 is communicated with a sludge filter bag 9 through a water pipe seven, a manual ball valve three and a pressure gauge two are installed on the water pipe seven, a gas input port of the gas-liquid mixing pump 13 is connected with an ozone generator 14 through a water pipe eight, a pressure gauge three is installed on the water pipe eight, a cooling input port and an output port of the ozone generator 14 are respectively connected with a water pipe nine and a water pipe ten, the water pipe nine is connected with the ceramic flat membrane 10 far away from the ozone generator 14, the other end of the water pipe ten is a tap water inlet 15, the tap water inlet 15 injects cooling liquid into the ozone generator 14 through the water pipe ten for circulation, the circulating cooling water is introduced into the ceramic flat membrane 10 through the water pipe nine, and a check valve II, a pressure gauge IV and an electromagnetic valve III are arranged at one end of the ceramic flat membrane 10 on the water pipe eleven.
The output port of the ceramic flat membrane 10 is connected with a standard water pump 11 through a water pipe twelve, a pressure protection switch is installed on the water pipe twelve, the output port of the standard water pump 11 is connected with a standard water tank 12 through a water pipe thirteen, an electromagnetic valve four is installed on the water pipe thirteen, and a liquid level switch two for detecting the height of the water level is arranged at the top of the standard water tank 12.
When the device is used, the experimental wastewater in the source water tank 1 is pumped out by the source water pump 2 and is led into the catalytic pool 3, the PE dosing device 4, the flocculating agent dosing device 5, the PAM dosing device 6 and the PAC dosing device 7 are controlled by the corresponding flow pumps according to specific purification requirements to lead out purified liquid medicine, the purified liquid medicine and the experimental wastewater are mixed and led into the catalytic pool 3, the liquid medicine and the experimental wastewater react with each other and are catalyzed and precipitated, impurities after precipitation are led into the sludge filter bag 9 by the sludge pump 8, sludge and the wastewater are filtered and separated from each other, the separated wastewater is led into the catalytic pool 3 again for cyclic purification, meanwhile, ozone generated by the ozone generator 14 is led into the catalytic pool 3 by the gas-liquid mixing pump 13, bacteria, viruses and the like in the catalytic pool 3 are purified, the reaction between the liquid medicine and wastewater impurities is catalyzed, cooling water is led into the tap water inlet 15 to carry out internal heat exchange and cooling on the ozone, then the wastewater is led out through a water pipe nine, and the purified water liquid in the catalytic pool 3 is led into a ceramic flat membrane 10 for filtration through a water pipe eleven, and finally is led into a standard water tank 12 under the pumping of a standard water pump 11, thus finishing the purification treatment of the wastewater.
The technical scheme includes that an intelligent PIC control system is adopted, the whole process computer automatically controls operation, a CPU receives/gives a liquid level signal to command a feed water pump to operate, meanwhile, the CPU automatically controls a flow pump to pump liquid into a catalytic pool 3 for static precipitation, then, a CPU commands a sludge pump 8 to send particles to a sludge filter bag 9 for filtration, the CPU simultaneously commands an ozone generator 14 and a gas-liquid mixing pump 13 to operate, after the command time is over, the CPU again commands the sludge pump 8 to send the particles to the sludge filter bag 9 for filtration, then, the CPU commands a standard water pump 11 to operate, the standard water quality is treated and sent to a standard water tank 12 through a ceramic flat membrane 10, and meanwhile, the CPU receives the liquid level signal of the standard water tank 12 to control the standard water pump.
The electrical components presented in the document are all electrically connected with an external master controller and 220V mains, and the master controller can be a conventional known device controlled by a computer or the like.
The utility model discloses a control mode comes automatic control through the controller, and the control circuit of controller can realize through the simple programming of technical staff in this field, and the supply also belongs to the common general knowledge in this field, and the utility model discloses mainly used protects mechanical device, so the utility model discloses no longer explain control mode and circuit connection in detail.
It is noted that, herein, relational terms such as first and second, and the like may be used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus. Without further limitation, an element defined by the phrase "comprising a reference structure" does not exclude the presence of other identical elements in a process, method, article, or apparatus that comprises the element.
Claims (5)
1. The utility model provides an experiment effluent disposal system, includes source water tank, its characterized in that: the water outlet of the source water tank is connected with an active water pump through a first water pipe, the output port of the source water pump is connected with a catalytic pool through a second water pipe, the second water pipe is sequentially communicated with a first branch pipe, a second branch pipe, a third branch pipe and a fourth branch pipe, the second water pipe is sequentially provided with a first manual ball valve, a first electromagnetic valve, a rotor type flowmeter and a pressure gauge from one end of the source water pump, and the tail ends of the first branch pipe, the second branch pipe, the third branch pipe and the fourth branch pipe are sequentially connected with a PE dosing device, a flocculating agent dosing device, a PAM dosing;
a drainage port on one side of the bottom of the catalysis tank is connected with a sludge pump through a water pipe III, the output end of the sludge pump is fixedly communicated with a sludge filter bag through a water pipe IV, a pressure gauge I is installed on the water pipe IV, a drainage port of the sludge filter bag is communicated with the catalysis tank through a water pipe V, a check valve I and an electromagnetic valve II are sequentially installed on the water pipe III from one end of the catalysis tank, and a manual ball valve II is installed on the water pipe IV;
the other water outlet on one side of the bottom of the catalysis tank is connected with a gas-liquid mixing pump through a water pipe six, one output port of the gas-liquid mixing pump is communicated with a sludge filter bag through a water pipe seven, a manual ball valve three and a pressure gauge two are installed on the water pipe seven, a gas input port of the gas-liquid mixing pump is connected with an ozone generator through a water pipe eight, a pressure gauge three is installed on the water pipe eight, a cooling input port of the ozone generator is connected with an output port of the ozone generator and is respectively connected with a water pipe nine and a water pipe ten, the water pipe nine is far away from the ozone generator and is connected with a ceramic flat membrane, the other end of the water pipe ten is a tap water inlet, the other input port of the ceramic flat membrane is communicated with the bottom of the catalysis;
the output port of the ceramic flat membrane is connected with a standard water pump through a water pipe twelve, a pressure protection switch is installed on the water pipe twelve, the output port of the standard water pump is connected with a standard water tank through a water pipe thirteen, and a solenoid valve four is installed on the water pipe thirteen.
2. An experimental wastewater treatment system according to claim 1, characterized in that: flow pumps are fixedly installed at the output liquid guide ports of the PE dosing device, the flocculating agent dosing device, the PAM dosing device and the PAC dosing device, and the output ports of the flow pumps are respectively communicated with a branch pipe I, a branch pipe II, a branch pipe III and a branch pipe IV which correspond to each other.
3. An experimental wastewater treatment system according to claim 1, characterized in that: and a tap water inlet injects cooling liquid into the ozone generator through a water pipe ten to circulate, and the circulated cooling water is introduced into the ceramic flat membrane through a water pipe nine.
4. An experimental wastewater treatment system according to claim 1, characterized in that: and a liquid level switch for detecting the height of the water level is arranged at the top of the source water tank.
5. An experimental wastewater treatment system according to claim 1, characterized in that: and a second liquid level switch for detecting the height of the water level is arranged at the top of the standard-reaching water tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922166698.5U CN211311151U (en) | 2019-12-05 | 2019-12-05 | Experiment effluent disposal system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922166698.5U CN211311151U (en) | 2019-12-05 | 2019-12-05 | Experiment effluent disposal system |
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| Publication Number | Publication Date |
|---|---|
| CN211311151U true CN211311151U (en) | 2020-08-21 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201922166698.5U Active CN211311151U (en) | 2019-12-05 | 2019-12-05 | Experiment effluent disposal system |
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|---|---|
| CN (1) | CN211311151U (en) |
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- 2019-12-05 CN CN201922166698.5U patent/CN211311151U/en active Active
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